Method for Producing Water Absorbent Resin Particle

ABSTRACT

The present invention provides a method for producing a water absorbent resin particle, in high productivity, not only in a controlled manner of particle size but also enhancing fundamental property (absorption capacity or absorption capacity against pressure) of a water absorbent resin. A method for producing a water absorbent resin particle having the cross-linking polymerization step for an aqueous solution of an unsaturated monomer; the grain refining step for water-swellable, water-containing gel-like cross-linked polymer (a) obtained in the cross-linking polymerization step; the drying step for grain refined gel; and the crushing step for a dried substance, wherein, in the grain refining step for the water-swellable, water-containing gel-like cross-linked polymer (a), water-swellable, water-containing gel-like cross-linked polymer (b), having solid content or centrifuge retention capacity different from solid content or centrifuge retention capacity of the cross-linked polymer (a) by equal to or larger than 1%, is subjected to coexistence.

TECHNICAL FIELD

The present invention relates to a method for producing a waterabsorbent resin, which is a water-swellable cross-linked polymer, andmore specifically the present invention relates to a method forproducing a water absorbent resin having a controlled particle size, andexcellent in fundamental property such as absorption capacity orextractables.

BACKGROUND ART

At present, a water absorbent resin (a water absorbing agent) such as across-linked polymer of a polyacrylate salt is widely used, aiming atabsorbing body fluid, as a constitution material of a hygienic articlesuch as a disposable diaper or a sanitary napkin, so-called anincontinence pad or the like.

Such a water absorbent resin is required to have excellent property suchas excellent fluid absorption amount or water absorption rate, gelstrength, gel fluid permeability in contacting with aqueous fluid suchas body fluid or the like, or excellent water suction force from asubstrate containing aqueous fluid. Furthermore, in recent essentialrequirements include a water absorbent resin powder having very narrowparticle size distribution, or a water absorbent resin powder havinghigh absorption capacity or low extractables, and also high absorptioncapacity against pressure or fluid permeability against pressure.

U.S. Pat. Re No. 32,649 has proposed a water absorbent resin excellentin gel strength, extractables and water absorption capacity; GBP No.2267094B has proposed a water absorbent resin excellent in fluidpermeability without load, water absorption rate and absorptioncapacity; technology specifying specific particle size distribution hasbeen proposed in U.S. Pat. No. 5,051,259, U.S. Pat. No. 5,419,956, U.S.Pat. No. 6,087,002, EP No. 0629441 or the like. In addition, there aremany proposals on water absorbent resins excellent in absorptioncapacity against pressure under various loads, or a measurement methodtherefor, and water absorbent resins with excellent absorption capacityagainst pressure only or other properties in combination have beenproposed in EP No. 0707603, EP No. 0712659, EP No. 1029886, U.S. Pat.No. 5,462,972, U.S. Pat. No. 5,453,323, U.S. Pat. No. 5,797,893, U.S.Pat. No. 6,127,454, U.S. Pat. No. 6,184,433, U.S. Pat. No. 6,297,335 andU.S. Pat. Re No. 37,021 or the like.

Among these properties, particle size has strong effect on otherproperties of a water absorbent resin, therefore, many methods forcontrolling particle size have been proposed. For example, as a methodfor controlling particle size, a method for recovering only a finepowder by separation, agglomeration or gelling has been proposed in U.S.Pat. No. 6,228,930, U.S. Pat. No. 4,950,692 (issued on Aug. 21, 1990),U.S. Pat. No. 4,970,267 (issued on Nov. 13, 1990), U.S. Pat. No.5,064,582 (issued on Nov. 12, 1991) or the like; a method forpolymerization of a powder of a water absorbent resin as a monomer hasbeen proposed in U.S. Pat. No. 5,432,899, U.S. Pat. No. 5,455,284, U.S.Pat. No. 6,867,269 or the like; and a method for agglomeration of all ofwater absorbent resins has been proposed in U.S. Pat. No. 4,734,478 andU.S. Pat. No. 5,369,148 or the like.

In addition, also a method for a polymerization or gel crushing tomaintain high productivity and property has been proposed in U.S. Pat.No. 6,906,159, US-2004-092688A, US-2004-234607A or the like.

However, trying to enhance property (for example, particle size control,enhancement of absorption capacity, reduction of water-extractables) ofa water absorbent resin by technique proposed in U.S. Pat. Re No.32,649, GBP No. 2267094B, U.S. Pat. No. 5,051,259, U.S. Pat. No.5,419,956, U.S. Pat. No. 6,087,002, EP No. 0629441, EP No. 0707603, EPNo. 0712659, EP No. 1029886, U.S. Pat. No. 5,462,972, U.S. Pat. No.5,453,323, U.S. Pat. No. 5,797,893, U.S. Pat. No. 6,127,454, U.S. Pat.No. 6,184,433, U.S. Pat. No. 6,297,335 and U.S. Pat. Re No. 37,021,accompanies, in many cases, reduction of productivity or use of sub-rawmaterials, and thus increase in production cost of a water absorbentresin is not desirable, in the viewpoint that a water absorbent resin isa disposable raw material of a diaper or the like.

Methods for controlling particle size proposed in U.S. Pat. No.6,228,930, U.S. Pat. No. 4,950,692, U.S. Pat. No. 4,970,267, U.S. Pat.No. 5,064,582, U.S. Pat. No. 5,432,899, U.S. Pat. No. 5,455,284, U.S.Pat. No. 6,867,269, U.S. Pat. No. 4,734,478 and U.S. Pat. No. 5,369,148provide still insufficient control of particle size, and furtheraddition of the new particle size controlling step (agglomeration orfine powder recovery) not only accompanied cost increase, but alsoprovided lowering of properties other than particle size, depending oncases. In addition, also in U.S. Pat. No. 6,906,159, US-2004-092688A andUS-2004-234607A, there was room for improvement.

DISCLOSURE OF THE INVENTION

Namely, the present invention has been made in view of the abovecircumstance. The present invention provides a method for producing awater absorbent resin particle, in high productivity, not only incontrolling particle size but also enhancing fundamental property (forexample, absorption capacity without load, absorption capacity againstpressure, extractables) of a water absorbent resin.

To solve the above problems, a production method of the presentinvention is a method for producing a water absorbent resin particlehaving the cross-linking polymerization step of an aqueous solution of awater-soluble unsaturated monomer; the grain refining step forwater-swellable, water-containing gel-like cross-linked polymer (a)obtained in the cross-linking polymerization step; the drying step forgrain refined gel; and the pulverizing and classifying step for a driedsubstance, wherein, in the grain refining step for the water-swellable,water-containing gel-like cross-linked polymer (a), water-swellable,water-containing gel-like cross-linked polymer (b), having solid contentor centrifuge retention capacity different from solid content orcentrifuge retention capacity of the cross-linked polymer (a), issubjected to coexistence.

According to the present invention, control of particle size (forexample, reduction of a fine powder) of a water absorbent resin isattained in low cost and in high productivity. In addition, it is alsopossible to enhance fundamental property (for example, absorptioncapacity without load, absorption capacity against pressure,extractables) of a water absorbent resin.

Further other objectives, features and advantages of the presentinvention will be clear by referring to preferable embodimentsexemplified in the following explanation.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a conceptual drawing of a gel grain refining apparatus (a meatchopper), which can be used in the present invention.

FIG. 2 is a schematic drawing of an arrangement structure of acontinuous polymerization apparatus and gel crusher, which is capable ofperforming a production method of the present invention.

FIG. 3 is a schematic drawing of a measurement apparatus of absorptioncapacity against pressure (AAP), which is used in the Examples.

DETAILED DESCRIPTION OF THE EMBODIMENT

Detailed explanation will be given below on the present invention,however, technical scope of the present invention should be determinedbased on description of claims, and should not be limited by thefollowing specific embodiments.

<<The Cross-Linking Polymerization Step>> (a) An Unsaturated Monomer

In the present invention, as an unsaturated monomer of a water absorbentresin, acrylic acid and/or a slat thereof are preferably used, andcontent thereof is preferably from 50 to 100% by mol, and morepreferably from 70 to 100% by mol and further preferably from 90 to 100%by mol, relative to total amount of the unsaturated monomer. Theabove-mentioned water absorbent resin is hereinafter called aspolyacrylic acid (salts)-based water absorbent resin or polyacrylic acid(salts)-based cross-linked polymer.

As the acrylate salt, a monovalent salt such as an alkali metal salt, anammonium salt or an amine salt or the like is included. Asneutralization rate, in the case where acrylic acid is neutralized withthe above salt, it is preferably from 30% by mol to 100% by mol, furtherpreferably from 50% by mol to 90% by mol, and particularly morepreferably from 60% by mol to 80% by mol. It should be noted that, theneutralization of acrylic acid may be carried out in advance at thestage of preparation of the unsaturated monomer before obtaining awater-containing polymer, and subsequently initiate a polymerizationreaction; or polyacrylic acid of the above cross-linked polymer obtainedduring polymerization or after completion of the polymerization reactionmay be neutralized; or they may be combined.

As a monomer other than acrylic acid used in the present inventionincludes, for example, a monomer exemplified in U.S. patents or Europeanpatents to be described later, and also includes specifically, forexample, a water-soluble or hydrophobic unsaturated monomer such asmethacrylic acid, maleic acid (anhydride), fumaric acid, crotonic acid,itaconic acid, vinylsulfonic acid, 2-(meth)acrylamide-2-methylpropanesulfonic acid, (meth)acryloxyalkane sulfonic acid and an alkaline metalsalt and an ammonium salt thereof; N-vinyl-2-pyrrolidone,N-vinylacetamide, (meth)acrylamide, N-isopropyl(meth)acrylamide,N,N-dimethyl(meth)acrylamide, 2-hydroxyethyl(meth)acrylate,methoxypolyethylene glycol (meth)acrylate, polyethylene glycol(meth)acrylate, isobutylene, lauryl(meth)acrylate or the like.

(b) An Inner Cross-Linking Agent

A method for cross-linking used in the present invention is notespecially limited, and includes for example, a post-cross-linkingmethod by the addition of a cross-linking agent during polymerization orafter the polymerization; a radical cross-linking method using a radicalpolymerization initiator; a radiation cross-linking method usingelectron beams or the like; or the like. It is preferable to polymerizeby the addition of a predetermined amount of an inner cross-linkingagent, in advance, to a monomer, and then subjecting to a cross-linkingreaction at the same time of polymerization or after polymerization.

As the inner cross-linking agent used in the present invention, one kindor two or more kinds of a polymerizable inner cross-linking agent suchas N,N′-methylenebisacrylamide, (poly)ethylene glycol di(meth)acrylate,(poly)propylene glycol di(meth)acrylate,(polyoxyethylene)trimethylolpropane tri(meth)acrylate,trimethylolpropane di(meth)acrylate, polyethylene glycoldi(β-acryloyloxypropionate), trimethylolpropanetri(β-acryloyloxypropionate), poly(meth)allyloxyalkane or the like; or areactive inner cross-linking agent with a carboxyl group, such aspolyglycidyl ether(ethylene glycol diglycidyl ether, or the like),polyol(ethylene glycol, polyethylene glycol, glycerin, sorbitol, or thelike) are used. It should be noted that, in the case where one or morekinds of inner cross-linking agents are used, it is preferable toessentially use the polymerizable inner cross-linking agent, inconsideration of absorption characteristics or the like of the resultingwater absorbent resin.

In view of property aspect, the inner cross-linking agent is used in arange of from 0 to 3% by mol, preferably from 0.005 to 2% by mol, morepreferably from 0.01 to 1% by mol, and further preferably from 0.05 to0.2% by mol, relative to the above monomer.

(c) An Aqueous Solution

In the present invention, cross-linking polymerization is carried out byusing an aqueous solution of an unsaturated monomer. In the case wherereversed phase suspension polymerization or aqueous solutionpolymerization is carried out in the polymerization step, an aqueoussolution containing the inner cross-linking agent is used, if necessary.Concentration of the unsaturated monomer component in this aqueoussolution (hereafter referred to as a monomer aqueous solution) is, inview of property aspect, preferably from 10 to 70% by weight, morepreferably from 15 to 65% by weight, and further preferably from 30 to55% by weight. It should be noted that a solvent other than water may beused in combination, if necessary, and kind of the solvent used incombination is not especially limited, however, alcohols such as methylalcohol, ethyl alcohol, n-propyl alcohol, isopropyl alcohol, n-butylalcohol, isobutyl alcohol, t-butyl alcohol, and the like areexemplified. The solvent used in combination is used, for example, in arange of from 0 to 50% by weight relative to the water.

Furthermore, various properties of a water absorbent resin may beimproved by the addition of a water-soluble resin and/or a waterabsorbent resin (particulate (spherical, amorphous, or crushed form)water absorbent resin or water absorbent resin of fine particles in anamount of, for example, from 0 to 50% by weight, preferably from 0 to20% by weight; or at least one kind selected from various foaming agents(a carbonate salt, an azo compound, air bubbles or the like), asurfactant, a chelating agent, and a chain transfer agent such ashypophosphorous acid (or a salt) or the like, in an amount of from 0 to5% by weight, preferably from 0 to 1% by weight, relative to themonomer, in polymerization.

(d) The Polymerization Step

In polymerization of the above aqueous solution of the unsaturatedmonomer, it is preferably carried out by aqueous solution polymerizationor reversed phase polymerization in view of performance aspect oreasiness of polymerization control. These polymerizations may be carriedout under air atmosphere, however, it is preferable to be carried outunder inert gas atmosphere such as nitrogen or argon (for example, underan oxygen concentration of equal to or lower than 1%), and a monomercomponent is preferably used for polymerization after sufficient purgingof dissolved oxygen with inert gas (for example, under an oxygenconcentration of below 1 ppm). In the present invention, continuous beltpolymerization, and continuous or batch kneader polymerization areincluded as particularly preferable aqueous solution polymerization,which is particularly suitable to aqueous solution polymerization, whichwas difficult to control polymerization, to obtain a water absorbentresin with excellent property in high productivity.

Aqueous solution polymerization is a method for polymerization of amonomer aqueous solution without using a dispersion solvent, and isdescribed in, for example, U.S. patents such as U.S. Pat. No. 4,625,001,U.S. Pat. No. 4,873,299, U.S. Pat. No. 4,286,082, U.S. Pat. No.4,973,632, U.S. Pat. No. 4,985,518, U.S. Pat. No. 5,124,416, U.S. Pat.No. 5,250,640, U.S. Pat. No. 5,264,495, U.S. Pat. No. 5,145,906, U.S.Pat. No. 5,380,808 or the like; and European patens such as EP No.0811636, EP No. 0955086, EP No. 0922717, EP No. 1178059, EP No. 1711541,EP No. 1799721 or the like. A monomer, a cross-linking agent, apolymerization initiator and other additives described in these patentsare also applicable to the present invention.

Among the above polymerization methods, high temperature polymerizationis preferable, wherein polymerization initiation temperature of theaqueous solution of the unsaturated monomer is equal to or higher than40° C., further preferably equal to or higher than 50° C., still furtherpreferably equal to or higher than 60° C., and particularly preferablyequal to or higher than 70° C. Application of the present invention towater-containing gel obtained by such high temperature polymerization(high temperature initiation polymerization) is capable of fulfillingeffect of the present invention including particle size control to themaximum extent possible. It should be noted that the upper limit isequal to or lower than boiling point of the aqueous solution, preferablyequal to or lower than 105° C.

In addition, high temperature polymerization (boiling polymerization) ispreferable, wherein peak temperature of polymerization temperature isequal to or lower than 95° C., more preferably equal to or lower than100° C. and further preferably equal to or lower than 105° C. (boilingpoint polymerization). Application of the present invention towater-containing gel obtained by such boiling temperature polymerizationis capable of fulfilling effect of the present invention includingparticle size control to the maximum extent possible. It should be notedthat the upper limit is sufficient to be equal to or lower than boilingpoint, preferably equal to or lower than 130° C., and further preferablyequal to or lower than 120° C. is sufficient.

It should be noted that polymerization time is also not especiallylimited, and may be determined as appropriate, depending on kind of ahydrophilic monomer or a polymerization initiator, reaction temperatureor the like, however, usually from 0.5 minute to 3 hours, and preferablyfrom 1 minute to 1 hour.

In polymerization of a monomer aqueous solution, for example, aredox-type initiator, wherein a polymerization initiator such as apersulfate salt such as potassium persulfate, ammonium persulfate,sodium persulfate; hydroperoxide such as t-butylhydroperoxide, hydrogenperoxide; azo compound such as 2,2′-azobis(2-amidinopropanedihydrochlorate salt; 2-hydroxy-1-phenyl-propane-1-one, benzoin methylether, or the like; and further a reducing agent such as L-ascorbicacid, which promotes decomposition of these polymerization initiators,are used in combination. Using amount of the polymerization initiator isusually in a range of from 0.001 to 1% by mol, further preferably from0.001 to 0.5% by mol, relative to the monomer.

In addition, instead of using a polymerization initiator, apolymerization reaction may be carried out by irradiation of activatedenergy beams such as radiation beams, electron beams, ultraviolet raysand the like to a reaction system; or by combination with radiationbeams, electron beams, an ultraviolet ray-sensitive polymerizationinitiator and the like; or by combination with the above polymerizationinitiators.

Rate of polymerization of the resulting water-containing gel-likecross-linked polymer (hereafter, water-containing gel) is preferably notless than 70% by mol, more preferably not less than 90% by mol andfurther preferably not less than 95% by mol. Most preferably, the rateof polymerization is further increased (preferably not less than 99% bymol, and further preferably not less than 99.9% by mol) by subsequentdrying step or the like.

<<The Grain Refining Step>>

The present invention is characterized in that, in the grain refiningstep for the water-swellable, water-containing gel-like cross-linkedpolymer (a) (hereafter may be referred to also as water-containing gel(a)), the water-swellable, water-containing gel-like cross-linkedpolymer (b), having solid content or centrifuge retention capacitydifferent from solid content or centrifuge retention capacity of thecross-linked polymer (a), is subjected to coexistence. Preferably, boththe cross-linked polymer (a) and the cross-linked polymer (b) are thepolyacrylic acid (salts)-based cross-linked polymer.

“The grain refining step” means a step of crushing gel.

Coexistence here indicates a state that the water-containing gel (a) andthe water-containing gel (b) are present together in a grain refiningapparatus, and suitably, the water-containing gel (a) and thewater-containing gel (b) are present together in a grain refiningapparatus during the grain refining step. For example, an embodimentthat the water-containing gel (a) and the water-containing gel (b) arestarted to be charged into the grain refining apparatus at the sametime, and end the charging at the same time; and an embodiment that thewater-containing gel (a) and the water-containing gel (b) are mixedbefore charging into the grain refining apparatus, and then charged intothe grain refining apparatus; are included. The mixture of thewater-containing gel (a) and the water-containing gel (b) may be carriedout continuously, semicontinuously or in batch-wise.

The explanation will be given in detail below on materials andapparatuses used in the grain refining step.

(The Water-Swellable, Water-Containing Gel-Like Cross-Linked Polymer(a))

In the present invention, the water-swellable, water-containing gel-likecross-linked polymer (a) obtained by the cross-linking polymerizationstep is subjected to grain refining before drying. Particle diameter(specified by a standard sieve) of the water-containing gel (a) afterthe grain refining is, in view of particle size control or propertyaspect, as mass median particle size, preferably from 0.1 to 20 mm, morepreferably from 0.5 to 10 mm and further preferably from 1 to mm.Preferably, not less than 95% by weight of the water-containing gel (a)has a particle size of not more than 25 mm. It should be noted that theclassification of the gel may be carried out in wet process withsolvent, or in dry process without solvent.

A shape of the water-containing gel (a) before the grain refining maytake various forms such as particulate, belt-like, plate-like,film-like, block-like one or the like, depending on a polymerizationmethod. In the present invention, the water-containing gel (a) in anyform can be subjected to grain refining, however, it is preferably abelt-like substance obtained by belt-polymerization or the like. It isbecause supplying belt-like gel to a gel grain refining apparatus (inparticular, a screw extruder to be described later) providesentanglement of the belt-like gel to a rotating blade, and is capable ofgrain refining efficiently. The belt-like water-containing gel (a) has athickness of preferably from 1 to 100 mm, and more preferably from 3 to50 mm, or from 4 to 20 mm. The thickness outside this range may providereduced property or difficulty in particle size control, in some cases.The belt-like water-containing gel (a) has a width of preferably from0.1 to 10 m, and more preferably from 0.5 to 5 m.

Solid content of the water-containing gel (a) subjected to the grainrefining is from 20 to 80% by weight, preferably from 30 to 70% byweight, further preferably from 40 to 75% by weight, and still furtherpreferably from 45 to 65% by weight. In the case where thewater-containing gel with a solid content within the above range isobtained after polymerization (if necessary, by the addition of water orby drying), crushing is possible by a method for grain refining(crushing) of the present invention. In particular, in the presentinvention, particles with a solid content of not less than 40% byweight, preferably not less than 45% by weight, more preferably not lessthan 50% by weight at the time of grain refining, are suitable inapplications, and enable particle size control. In the presentinvention, “solid content” means rate of solid content (% by weight) inwater-containing gel, and as “solid content”, value determined by amethod described in Examples, to be described later, is adopted.

In the present invention, such a method is preferably used that anunsaturated monomer such as acrylic acid or the like, a polymerizationinitiator and an aqueous alkaline solution for neutralization of theunsaturated monomer are continuously mixed and stirred to prepare amonomer solution, followed by polymerization in a short time bycontinuously supplying this onto a belt, by utilization ofneutralization heat and polymerization heat, to continuously obtain thebelt-like water-containing gel (a). Preferable temperature of a monomeraqueous solution or polymerization temperature is in the above-describedrange (the above high temperature initiation polymerization).

Preferably temperature of the water-containing gel (a) at the time ofgel grain refining is, in view of particle size control or propertyaspect, usually equal to or higher than 40° C., preferably from 40 to120° C., more preferably from 50 to 100° C., and particularly preferablyfrom 60 to 90° C. To maintain at such temperature, temperature ofpolymerization may be controlled, or polymer gel after polymerizationmay be subjected to heat insulation or heating, if necessary. In thecase where the water-containing gel (a) at the time of gel grainrefining has temperature higher than the above range, it may besubjected to heat radiation or cooling, while in the case where thewater-containing gel (a) has temperature lower than 40° C., thewater-containing gel (a) is preferably subjected to heating to equal toor higher than 40° C. A method for heating the above water-containinggel (a) (or water-containing gel (b) to be described later) is notespecially limited, and various heating apparatuses may be used.

It is preferable a grain refining step that the water-containing gel (a)and the water-containing gel (b) coexist is carried out withinpreferably one hour, more preferably ten minutes, further preferably oneminute after the water-containing gel (a) is taken from the apparatusused for polymerization, because the above mentioned preferabletemperature range in gel grain refining is maintained.

(The Rough Crushing Step)

It should be noted that the rough crushing step, wherein particles arecrushed roughly (rough crushing), may be carried out before the abovegrain refining step. This rough crushing of the water-containing gel (a)makes easy not only supply of the water-containing gel (a), but alsofilling into a grain refining apparatus to be described later, andenables to more smoothly carry out the grain refining step. As a roughcrushing method used in the above rough crushing step, one, which iscapable of rough crushing without kneading the water-containing gel, ispreferable, and includes, for example, a guillotine cutter or the like.

A size or shape of a rough crushed product of the water-containing gelobtained in the rough crushing step differs by a method forpolymerization used, therefore not especially limited, as long as beingthe size or shape in a degree enabling filling into the grain refiningapparatus, however, in general, the size or shape of a rough crushedproduct of the water-containing gel (a) has a length of a longer sidepart thereof of preferably from 5 to 500 mm, more preferably from 10 to150 mm, and further preferably from 30 to 100 mm. The length of theabove side below 5 mm does not have meaning for crushing by the grainrefining apparatus, while the length of the above side over 500 mmeasily generates large clearance in filling the water-containing gelinto the grain refining apparatus, and could reduce crushing efficiency.

(The Water-Swellable, Water-Containing Gel-Like Cross-Linked Polymer(b))

Explanation will be given below on the water-swellable, water-containinggel-like cross-linked polymer (b). It should be noted that thewater-containing gel is one containing water and in a swollen state,however, embodiments containing a solvent other than water (hydrophilicsolvent, for example alcohols such as methyl alcohol, ethyl alcohol,n-propyl alcohol, isopropyl alcohol, n-butyl alcohol, isobutyl alcohol,t-butyl alcohol, and the like) may be possible. In this case, thesolvent other than water is preferably from 0 to 50% by weight, relativeto water.

In the present invention, such a method is suitably used that after theaddition of the water-containing gel (b) to the water-containing gel (a)before grain refining, the water-containing gel (a) and thewater-containing gel (b) are continuously extruded by a grain refiningapparatus (preferably a screw extruder) in a state that compressionforce at the vicinity of extrusion exit of the above screw extruder isenhanced. In this way, the treated amount is enhanced, the particle sizeof a water absorbent resin is also more controlled and preferably,fundamental properties (For example, after-mentioned absorptioncapacity, extractables and the like) are also improved as compared withthe case where only the water-containing gel (a) is used.

Conventionally, in crushing, to prevent generation of kneading or mutualadhesion of crushed substances, an adhesion prevention agent such assilicone oil or the like, or sticking prevention agent such as asurfactant was added to a water-containing gel-like polymer. However,such a surfactant reduces absorption performance, due to reducingsurface tension of the water-containing gel-like polymer, and siliconeoil or the like reduces water absorbing characteristics due tolipophilic nature thereof, resulting in a cause of reducing quality of awater absorbent resin. According to the present invention, a waterabsorbent resin excellent in safety, without influence of the additives,even when used in a disposable diaper or a sanitary article, can beproduced, by using a conventional simple apparatus and by using thewater-containing gel (b) as an additive, and by carrying out efficientcrushing, wherein kneading or mutual adhesion of crushed substances isprevented.

Crushing of water-containing gel using a screw extruder has been known,however, various adhesion prevention agents or sticking preventionagents have been added to prevent kneading or mutual adhesion during thecrushing. However, supplying the water-containing gel (b), in crushing awater-containing polymer using a screw extruder, is capable ofpreventing kneading or mutual adhesion. Therefore, in the presentinvention, it is not necessarily required to add a surfactant, or anadhesion prevention agent such as silicone oil, and in view of propertyimprovement of a water absorbent resin, adding amount of the surfactantand the adhesion prevention agent is preferably from 0 to 5% by weight,more preferably equal to or lower than 3% by weight, and furtherpreferably equal to or lower than 1% by weight, relative to 100% byweight of the water-containing gel (a).

In the present invention, solid content or centrifuge retention capacitybetween the water-containing gel (a) and the water-containing gel (b) isdifferent. The difference in solid content between the water-containinggel (a) and the water-containing gel (b) is preferably from 1 to 60,preferably from 2 to 55, more preferably from 2 to 50 in terms ofimprovement of property. “Difference in solid content” means absolutevalue of value that solid content of the water-containing gel (a) minussolid content of the water-containing gel (b). For example, in Example1, difference in solid content is “3”, because solid content of thewater-containing gel (a) is 53.0% by weight, and solid content of thewater-containing gel (b) is 50.0% by weight.

One preferable embodiment of the water-containing gel (b) is thewater-containing gel (b2) having low solid concentration. In such anembodiment, the solid concentration is preferably equal to or lower than10% by weight, more preferably equal to or lower than 5% by weight, andfurther preferably equal to or lower than 2% by weight. A certain degreeof low solid concentration of the water-containing gel (b), namely to below viscosity, fulfills roles of a lubricant by the water-containing gel(b), and suppresses mutual adhesion of the water-containing gel (a), orgeneration of kneading caused by sticking. In view of adhesionprevention or sticking adhesion, solid content of the water-containinggel (b) is preferably lower as compared with the water-containing gel(a). In addition, the lower limit of the solid content of thewater-containing gel (b) is not especially limited, however, in view ofreduction of fine particles, it is preferably not less than 0.1% byweight, more preferably not less than 0.3% by weight, and furtherpreferably not less than 0.5% by weight. The water-containing gel (b2)having the same composition as that of the water-containing gel (a), butlower sold concentration is suitably used, and specifically, it can beobtained by the addition of water to the water-containing gel (a)obtained by the cross-linking polymerization step. Such an embodiment isvery efficient in view of production, and also preferable in view ofproperty due to having the same component. It should be noted that,different from the water-containing gel (b1) to be described later,effect of the water-containing gel (b2) does not depend on particlediameter of a cross-linked polymer before containing water; for example,even in water-containing gel of a cross-linked polymer composed of fineparticles equal to or smaller than 150 μm, or water-containing gel ofthe water-containing gel (a) obtained by the cross-linkingpolymerization step, effect of the present invention is similar, as longas solid content is within the above range.

In addition, a further other preferable embodiment of thewater-containing gel (b) is the water-containing gel (b1) obtained bythe addition of water to a water absorbent resin fine powder. Here, “afine powder” indicates that not less than 90% by weight of a powder hasa particle diameter of preferably less than 212 μm, more preferably lessthan 180 μm, and further preferably less than 150 μm. One having aparticle diameter less than 150 (180, 212) μm indicates one passingthrough a JIS standard sieve of 150 (180, 212) μm. The water-containinggel (b1), similarly to the water-containing gel (b2), not only fulfillsrole of a lubricant, but also reduces the fine powder of a waterabsorbent resin produced from the water-containing gel (a), and alsoimproves uniformity of a water-containing gel mixture by being mixed ina grain refining apparatus.

Solid content in the water-containing gel (b1) is preferably from 10 to70% by weight, more preferably from 20 to 60% by weight and furtherpreferably from 30 to 60% by weight. It should be noted that effect ofthe present invention can be fulfilled even when solid of content thewater-containing gel (b1) is a little higher, as compared with theabove-described water-containing gel (b2); this is because, in the caseof the fine particle, gel viscosity is low even when solid contentthereof is high in a certain degree, and is capable of fulfilling a roleof a lubricant among the water-containing gel (a) itself.

Namely, the water-containing gels (b2) and (b1) form a group aswater-containing gel having low viscosity, and such water-containing gelhaving low viscosity acts as a lubricant suppresses mutual adhesion orsticking in crushing of the water-containing gel (a) and fulfills effectof the present invention.

In addition, a difference in centrifuge retention capacity between thewater-containing gel (a) and the water-containing gel (b) is preferably1 to 20 g/g, more preferably 2 to 15 g/g. It should be noted thatabsorption capacity (centrifuge retention capacity, CRC, per solidcontent) of the water-containing gel (a) is preferably from about 10 to40 g/g. In the present invention, as centrifuge retention capacity (CRC)of water-containing gel, value determined by a method described inExamples to be described later is adopted, for a cross-linked polymer(solid content) in water-containing gel.

Centrifuge retention capacity of the water-containing gel (b) ispreferably lower as compared with the water-containing gel (a);preferably lower by from 1 to 20 g/g, and further preferably lower byfrom about 2 to 15 g/g, as difference in centrifuge retention capacity(CRC).

The water-containing gel (b) is preferably produced from a waterabsorbent resin, which should be disposed in the production step of awater absorbent resin. Not only by being capable of recycling asubstance to be originally disposed, but also by using a water absorbentresin, to be disposed, in the grain refining step, effect of reducingfine particles of a water absorbent resin is provided. Specifically, thefollowing (b1) or (b2) is used.

(b1) Water-Containing Gel Obtained by the Addition of Water to a WaterAbsorbent Resin Powder

As an example, the water-containing gel (b), which is obtained by theaddition of water to a water absorbent resin powder after theclassification step, is preferable. In the classification stepsubsequent to the drying step and the crushing step, only particleswithin the predetermined range are selected to make a water absorbentresin. A classification method here is also not especially limited, anda sieve or the like is suitably used. For example, in the case where thesize of a crushed product is set to be in a range of from 212 to 850 μm,the crushed product is classified first, in advance, with a sieve of 850μm, and then sieved the crushed product, which passed through the abovesieve, with a sieve of 212 μm. A crushed product remaining on this sieveof 212 μm is a water absorbent resin within a desired range.

A water absorbent resin particle used in the water-containing gel (b)includes, as described above, a fine powder classified in the productionstep of a water absorbent resin, for example, the above classificationstep; a fine powder generating in the surface cross-linking step to bedescribed later or the transportation step of a water absorbent resin; afine powder captured in a bag filter in the crushing step; or the like,however, preferably a fine powder obtained by classification before orafter the surface cross-linking step. In addition, a fine powder of awater absorbent resin, generating at the other production line or in aplant, may be used. The fine powder may be in a dried state or in a wetstate, however, water content of the fine powder is preferably from 0 to15% by weight, more preferably from 0 to 10% by weight, and particularlypreferably from 0 to 5% by weight.

A fine powder with a particle diameter of less than 150 μm (or less than212 μm; specified by a standard sieve), when used as a water absorbentresin, reduces property or handling property thereof. Specifically, iteasily generates dust during work, deteriorates work environment, causesclogging, and in water absorption, easily generates an agglomerate(lump) and results in to inhibit diffusion of fluid. On the other hand,disposal of this fine powder as it not only requires cost or additionalwork for disposal, but also reduces yield in a water absorbent resin.Therefore, as a water absorbent resin powder used in thewater-containing gel (b), it is very preferable that a fine powderpreferably having a particle diameter of smaller than 212 μm, morepreferably a particle diameter of smaller than 180 μm, and furtherpreferably a particle diameter of smaller than 150 μm, is recovered forreuse. A particle diameter of smaller than 150 (180, 212) μm indicatesone passing through a JIS standard sieve of 150 (180, 212) μm.

Solid content in the water-containing gel (b1), obtained by the additionof water to a water absorbent resin powder, is preferably from 10 to 70%by weight, more preferably from 20 to 60% by weight, and furtherpreferably from 30 to 60% by weight.

(b2) Water-Containing Gel Obtained by the Addition of Water to PolymerGel of a Water Absorbent Resin

The above water-containing gel (b) is preferably obtained in the washingstep with water of a production apparatus of a water absorbent resin.The washing step with water indicates the step for cleaning a productionapparatus of the water absorbent resin after completion of production ofthe water absorbent resin. A production apparatus such as apolymerization apparatus or a gel crusher adhered with gel iscontinuously or in batch-wise washed with water, and the resulting gelor a dispersed substance in water may be used as it is as thewater-containing gel (b). Namely, the water-containing gel (b2) ispreferably water-containing gel having reduced solid content by theaddition of water to polymer gel obtained in the cross-linkingpolymerization step. As a preferable embodiment, water-swollen gelobtained by continuously washing a belt with water, after peeling abelt-like gel in continuous belt polymerization, may be used as thewater-containing gel (b).

The water-containing gel (b2) obtained in the above washing step withwater is usually in a saturated-swollen state, therefore, solid contentthereof is from 0.1 to 10% by weight, further from 0.3 to 5% by weight,and particularly from about 0.5 to 2% by weight, and is obtained withdifferent solid content as compared with the water-containing gel-likecross-linked polymer (a) within a suitable range of the presentinvention. Use of the water-containing gel (b) having such low solidcontent is capable of providing uniform crushing of the water-containinggel (a) obtained in polymerization, and attaining particle size controlor improvement of property of a water absorbent resin after drying. Inaddition, use of the water-containing gel (b2) is capable of suppressingadhesion of gel inside a grain refining apparatus onto the apparatus,and thus improving self-cleaning capability.

The water-containing gel (b), likewise the water-containing gel (a), isone wherein an unsaturated monomer is subjected to cross-linkingpolymerization. As the unsaturated monomer used for the water-containinggel (b), the same one as described in the above the water-containing gel(a) is used. It is preferable that composition of the unsaturatedmonomer is the same as in the water-containing gel (a) (preferablypolyacrylic acid (salts)-based cross-linked polymer), in view ofproperty of the resulting water absorbent resin.

(Using Amount)

The water-containing gel (b) is supplied to a grain refining apparatustogether with the water-containing gel (a), however, supplying amountthereof is not especially limited, and differs depending on theembodiments of the water-containing gel (b). For example, in the case ofthe water-containing gel (b2) having low solid concentration, preferablythe water-containing gel (a): the water-containing gel (b)=100: from0.001 to 100, more preferably 100: from 0.001 to 50, in weight ratio. Inaddition, in the case of the fine powder of water-containing gel (b1),the ratio is preferably 100: from 0.1 to 50, and more preferably 100:from 0.1 to 30. To be within such a range is capable of sufficientlyfulfilling effect of the addition of the water-containing gel (b), andbeing less possible to generate kneading during crushing. In addition,it also does not require excess quantity of thermal energy or dryingtime in drying the crushed substance, and also provides less reductionof property of a water absorbent resin.

Solid content of a mixture of the water-containing gel (a) and thewater-containing gel (b) is preferably from 30 to 70% by weight, morepreferably from 40 to 60% by weight, further preferably from 45 to 55%by weight. Temperature after mixing or after grain refining is alsopreferably within a range for the above water-containing gel (a).

(A Grain Refining Apparatus)

As a grain refining apparatus (a gel crusher) to be used, such one ispreferably used that is classified to a shear rough crusher, an impactcrusher, a high speed rotation type crusher, among crushers namesclassified in Table 1.10 of Powder Engineering Handbook (edited byPowder Engineering Association, 1^(st) edition), and has one or moremechanisms in crushing mechanism such as cutting, shearing, impacting,friction or the like; among crushers corresponding to such machinetypes, a crusher having cutting and shear mechanism as main mechanism isparticularly preferably used.

As a crusher type name, a crusher is classified into a roll rollingtype, and a roll mill (roll rotation type), and as for one having acompression mechanism as a crushing mechanism, those having strong shearand cutting effect can be used, however, those having weak shear andcutting effect but strong compression effect may not be used in certaincases. In addition, a crusher type such as a compression crusher, apowder layer hammering type or the like is not used, because acompression mechanism is a main crushing mechanism, by which awater-containing polymer is hardly fractured by compression. Inaddition, a crusher type such as an autogenous mill or a ball mediummill is also not used, because of not substantially having a shear orcutting mechanism.

A specific example of a crusher or a cutting-shearing mill, which can beused in the present invention, is listed below.

VERTICAL CUTTING MILL, manufactured by Orient, Inc.

ROTOPLEX, manufactured by Hosokawa Micron Corp.,

TURBO CUTTER, manufactured by Turbo Kogyo Co., Ltd.

TURBO GRINDER, manufactured by Turbo Kogyo Co., Ltd.

TYRE SHREDDER, manufactured by Masuno Seisakusyo, Ltd.

ROTARY CUTTER MILL, manufactured by Yoshida Seisakusyo Co., Ltd.

CUTTER MILL, manufactured by Tokyo Atomizer manufacturing Co., Ltd.

DISC MILL, manufactured by PALLMANN Maschinenfabrik GmbH & Co.)

SHRED CRUSHER, manufactured by Tokyo Atomizer manufacturing Co., Ltd.

CUTTER MILL, manufactured by Masuko Sangyo Co., Ltd.

CRUSHER, manufactured by Masuko Sangyo Co., Ltd.

ROTARY CUTTER MILL, manufactured by Nara Machinery Co., Ltd.

GAINAX CRUSHER, manufactured by Hourai Corp.

U-COM, manufactured by Hourai Corp.

MESHMILL, manufactured by Hourai Corp.

DISC CUTTER, manufactured by Hourai Corp.

Among these grain refining apparatuses, a continuous or a batch-typekneader, shredder, meat chopper, “Dome Gran” or the like can beexemplified. For example, meat chopper is one for grain refining(crushing) by extruding water-containing gel from a porous plate, and asan extrusion mechanism, a system for pressure feeding water-containinggel from a supply port thereof to the porous plate, such as a screw typeone or a rotating roll type one or the like is used. A screw typeextruder may have a single-axis or a multi-axis, and may be one usuallyused for extrusion molding of meat, rubber, or plastics; or one used asa crusher.

A grain refining apparatus preferably used in the present invention is ascrew extruder, which is available in low price, compact and simple inoperation. Supplying a water-containing polymer using a screw extruderprovides continuous entanglement of a belt-like substance onto arotating blade, and thus the substance is transferred to the porousplate side while being crushed.

A grain refining apparatus preferably used in the present invention is ascrew extruder having function of transferring a substance in an axisdirection by a screw rotation in a static barrel. In the presentinvention, as a screw extruder, any screw number of a single screw, twinscrew, or four screw or the like may be used, as long as being anapparatus having a porous plate and a rotating blade for grain refiningwater-containing gel to an optimal size, and screw(s) for transferringwater-containing gel to the above porous plate, which are built-in acasing having a supply port of water-containing gel as a target of grainrefining, and an extrusion port of a crushed substance. In addition,rotation direction of the twin screw may be any of co-rotational orcounter-rotational direction. What is called a meat chopper or a screwextruder or the like is included.

In the porous plate or porous plane (for example, sphere-like one) toextrude the water-containing gel (a), pore diameter thereof preferablyhas a porous pore structure of from 0.3 to 25 mm. A pore shape is notespecially limited, and includes circular form; four-way type such assquare and rectangle; triangle, hexagon or the like, however, a circularhole is preferable for extrusion. It should be noted that, the abovepore diameter is specified by diameter wherein the outer circumferenceof the mesh opening part is converted to the outer circumference of acircle. The pore diameter is preferably from 2 to 20 mm and furtherpreferably from 5 to 15 mm. The pore diameter of the porous structuresmaller than 0.3 mm may bring about string-like gel, or makes gelextrusion impossible. The pore diameter of the porous structure largerthan 25 mm could not fulfill effect of the present invention. It shouldbe noted that number of holes of the porous plate is determined asappropriate depending on size of the porous plate or the porous plane,and the hole may be one per porous plate, however, usually equal to ormore than two, further from 3 to 10,000 and more preferably from 5 to5,000. The number of porous plate per apparatus may be one, or pluralnumber.

In addition, thickness of the above pore plate 17 (FIG. 1) is within arange of from 1 to 20 mm. Opening rate of the above pore plate ispreferably from 20 to 55%, more preferably from 25 to 35%, andparticularly preferably from 27 to 33%. The opening rate below 20% makesextrusion of water-containing gel difficult, and thus reducesproductivity. In addition difficulty in extruding water-containing gelprovides excessive grain refining of water-containing gel at a pressurefeed region to the porous plate, and thus not preferable. On the otherhand, the opening rate over 55% results in insufficient addition ofcompression force to water-containing gel and could provide insufficientdispersion of water-containing gel. It should be noted that the aboveopening rate indicates ratio of total area of all pores to total area ofthe porous plate (substantially, regarded as the same as cross-sectionalarea of the casing). An apparatus having the above porous plate, porediameter and opening rate thereof set as described above is capable ofadding large compression force to water-containing gel charged into ascrew extruder, at the vicinity of the extrusion port.

It should be noted that, in the present invention, to improve mixingcapability of fine powders or particle size control of grain refinedwater-containing gel, screw extruders may be combined in a multi-stepway, or the same extruder may be used for multiple extrusions.

(A Screw Extruder)

As a grain refining apparatus preferably used in the present invention,a screw extruder is included, and explanation will be given belowfurther thereon.

As a screw extruder, one equipped with the following configuration, forexample, as shown in FIG. 1, is suitably used: the casing 11, themounting 12, the screw 13, the supply port 14, the hopper 15, theextrusion port 16, the porous plate 17, the rotating blade 18, the ring19, the back-flow prevention member 20, the motor 21, the belt-likeprotrusion 22 or the like.

The above casing 11 takes a cylinder-like shape, arranged with the screw13 along a longitudinal direction of the casing 11 inside thereof. Atthe one end of the cylinder-like casing 11, the extrusion port 16 isinstalled to crush water-containing gel by extrusion, and at the otherend, the motor 21 or a drive system for rotating the screw 13 isinstalled. At the lower part of the casing 11, the mounting 12 isinstalled, by which a screw type extruder can be arranged stably at thefloor. On the other hand, at the upper part of the casing 11, the supplyport 14 for supplying water-containing gel is installed, and preferably,the hopper 15 is installed to easily supply water-containing gel.

A shape or size of the above casing 11 is not especially limited, aslong as having a cylinder-like inner surface so as to correspond to ashape of the screw 13. In addition, rotation number of the screw 13 isnot especially limited because it differs as appropriate depending onthe shape of a screw extruder, however, as will be described later, itis preferable that rotation number of the screw 13 is changed accordingto supplying amount of water-containing gel. The rotation number is, forexample, from 1 to 1000 rpm, further from 10 to 500 rpm.

Rotation direction of the above screw 13 is not especially limited. Inthe present invention, the above screw 13 is set to rotate clockwiseviewed from the end part of a side connecting the motor 21.

At the above extrusion port 16, the porous plate 17, having a pluralityof the holes 17 a, is arranged. In addition, this porous plate 17 isfixed to the extrusion port 16 in a detachable manner by the ring 19. Itis because diameter of the holes 17 a of the porous plate 17 determinesparticle size of grain refined water-containing gel, and therefore theporous plate 17 with different diameter of the holes 17 a must beexchanged to adjust particle size of water-containing gel.

One embodiment of the present invention will be shown below. As shown inFIG. 1, water-containing gel (a) and water-containing gel (b) chargedfrom the supply port 14 into the casing 11 are not mixed sufficiently.Water-containing gel (a) and water-containing gel (b) charged into thecasing 11 are mixed (kneaded) by rotation of the screw 13, however,rotation of this screw 13 transfers rather than mixing them toward theextrusion port 16 side, resulting in adding external force towater-containing gel (a). Therefore, uniform compression force is addedin a degree so that water-containing gel (a) is not compressed. Itshould be noted that most parts inside the casing 11, wherein suchuniform compression force is added to water-containing gel (a), is setas a uniform compression zone, as shown in FIG. 1.

On the other hand, at the extrusion port 16, the porous plate 17 isarranged, and therefore water-containing gel (a) is not extruded soeasily at the vicinity of the extrusion port 16, and is compressed byrotation of the screw 13. Furthermore, as described-above,water-containing gel (a) and water-containing gel (b) in the casing 11are transported toward the extrusion port 16 side by rotation of thescrew 13, which further increases compression force. As a result,water-containing gel (a) and water-containing gel (b) are stirred andmixed while being compressed (see FIG. 1) and extruded from theextrusion port 16 (the porous plate 17). It should be noted that thevicinity of the extrusion port 16, wherein such large compression forceis added, is set as a compression zone, as shown in FIG. 1.

In usual stirring and mixing, water-containing gel (a) andwater-containing gel (b) are not compressed (see the uniform compressionzone in FIG. 1), therefore water-containing gel (b) added towater-containing gel (a) is not sufficiently dispersed, and easilybecomes an agglomerate (lump). On the other hand, stirring and mixing bythe above screw type extruder, water-containing gel (a) andwater-containing gel (b) are mixed under compression, thereforewater-containing gel (b) is stirred in a state of closely adhered towater-containing gel

(a) (See the Compression Zone in FIG. 1).

Furthermore, the above-described screw extruder used in the presentinvention is preferably equipped with the back-flow prevention member 20at least at the vicinity of the extrusion port 16. Therefore, theaddition of further more sufficient compression force is possible to beadded at the vicinity of the extrusion port 16. Equipment of the aboveback-flow prevention member 20 at the vicinity of the extrusion port 16(the porous plate 17) prevents back-flow of water-containing gel (a)toward the supply port 14, even when diameter of the hole 17 a is rathersmall. Therefore, the addition of further more sufficient compressionforce to the water-containing gel at the vicinity of the extrusion port16 not only ensures dispersion and mixing of water-containing gel (b)but also carries out smooth extrusion of water-containing gel (a), whichis capable of avoiding reduction of productivity.

A shape of the back-flow prevention member 20 is not especially limited,as long as one preventing back-flow of water-containing gel (a) from theextrusion port 16 toward the supply port 14 side. For example, as theback-flow prevention member 20, a helical belt-like protrusion 20 a asshown in FIG. 1, a concentric circular and belt-like protrusion 20 b, orthe belt-like protrusion 22 in parallel to a forward direction of thescrew 13 (see FIG. 1), a protrusion with a particulate, spherical orhorn-like shape, or the like is included.

Clearance of the back-flow prevention member 20 and the screw 13 ispreferably within a range of from 0.1 to 5 mm. The clearance below 0.1mm inhibits rotation of the screw 13 by the back-flow prevention member20, and thus not preferable. On the other hand, the clearance over 5 mmis not capable of preventing back-flow of water-containing gel by theback-flow prevention member 20 and thus not preferable.

At the vicinity of extrusion port 16, the end part of the screw 13, atthe side not connected to the motor 21, is present, however, between theabove porous plate 17 and the end part of the above screw 13, the aboverotating blade 18 is arranged, so as to rotate by substantiallycontacting with the surface of the porous plate 17. Use of this rotatingblade 18 makes particles of water-containing gel, which are extrudedfrom the porous plate 17, smaller and is capable of making more uniformparticle size distribution.

Configuration of the rotating blade 18 is not especially limited, andfor example, one having configuration of a cross type may be suitablyused. In addition, rotation direction of this rotating blade 18 is alsonot especially limited, and for example, in the present invention, therotating blade 18 is set to rotate in the same direction as that of thescrew 13. Furthermore, rotation number of the rotating blade 18 is alsonot especially limited.

Variation width of rotation number of the above screw 13, responding tochange of supplying amount of water-containing gel is also not limitedto special width, and optimal variation width may be specified byconditions of grain refining, for example, a shape of a screw extruderto be used (volume of the casing 11 or a shape of the screw 13, diameterof the hole 17 a of the porous plate 17 or the like) or property ofwater-containing gel or the like. Therefore, the above rotation numberis preferably specified as appropriate corresponding to a screw typeextruder or water-containing gel to be used.

(Grain Refining Conditions)

The present inventors have found that time for gel to pass throughinside a grain refining apparatus is an important factor in settinggrain refining conditions, in the case where the water-containing gel(a) and the water-containing gel (b) are coexistence inside the grainrefining apparatus. Furthermore, the present inventors have also foundthat it is preferable for gel to rapidly pass inside the apparatus toreduce a fine particle of finally obtained water absorbent resin.Detailed mechanism therefor is not clear, however, for gel to rapidlypass inside the apparatus is considered to reduce a fine particle of awater absorbent resin because of reduction of kneaded water-containinggel (a).

Explanation will be given on a screw extruder, as a preferableembodiment, with reference to FIG. 1; time for gel to pass throughinside a grain refining apparatus is defined as time for gel to passthrough inside the casing 11 of FIG. 1. In the present invention,residence time of gel represented by the following formula is used astime for gel to pass through inside the casing: residence time of gel(sec)=(residence amount of gel (kg)/charging amount of gel (kg/h))×3600(sec/h). It should be noted that as residence amount of gel and chargingamount of gel, values used in Examples are adopted.

The residence time of gel is preferably over 0 and equal to or shorterthan 30 seconds, more preferably equal to or shorter than 25 seconds,further preferably equal to or shorter than 20 seconds and particularlypreferably equal to or shorter than 15 seconds, in view of reducing afine particle.

(Additives Other than Water)

In addition, in the present invention, other additives may be added towater-containing gel or a water absorbent resin.

Namely, to furnish various functions, an oxidizing agent; a reducingagent such as a (b1) sulfite salt or the like; a chelating agent such asan aminocarboxylic acid; water-insoluble inorganic or organic powdersuch as silica or metallic soap or the like; a deodorant, anantimicrobial agent, polyamine, pulp, or thermoplastic fiber or the likemay be added to a water absorbent resin, as additives, in an amount offrom 0 to 3% by weight and preferably from 0 to 1% by weight.

It should be noted that the above-described additives are referred to indetail in WO2006/109844, and these descriptions are also appliedcorrespondingly to the present invention. Among these additives,chelating agents exemplified in U.S. Pat. No. 6,599,989, U.S. Pat. No.6,469,080 or the like are preferably contained in a water absorbentresin, in an amount of preferably from 0.001 to 3% by weight and morepreferably from 001 to 2% by weight.

<<The Drying Step>>

Grain refined gel obtained by the grain refining step is then subjectedto the drying step, the crushing step, and the classification step asdescribed above to yield a particulate water absorbent resin having asize of the predetermined range. It should be noted that the fine powderobtained after the crushing step, and the classification step ispreferably reused by a method described above again.

For drying, a usual dryer or a heating furnace may be used. For example,an air-flow band dryer, a stirring dryer, a rotating dryer, a diskdryer, a fluidized bed dryer, an air-flow dryer, an infrared ray dryer,a microwave drying, a hot air drying, an infrared drying, a drum dryerdrying, a stirring drying method or the like may be adopted. In thepresent invention, to prevent generation of a fine powder caused byphysical fracture or friction of a dried substance, a drying method byhot air or the like, without moving a drying object, such as an air-flowband dryer, is preferable.

Drying temperature or drying time differs by a drying system, however,usually from 100 to 250° C. for from 3 to 120 minutes are sufficient. Adried substance obtained in this way has a solid content of usually from85 to 99% by weight, and preferably from 90 to 98% by weight (dryingloss at 180° C. for 3 hours).

(The Pulverizing Step)

A water absorbent resin is crushed after the drying step (thepulverizing step). A method for pulverizing here is also not especiallylimited, and the above dried substance may be subjected to pulverizingby a vibration mill, a roll granulator, a knuckle type crusher, a rollmill, a high speed rotation type crusher, a cylinder-like mixer or thelike.

In the present invention, to reduce generation of a fine powder of awater absorbent resin, content of the fine powder in a water absorbentresin is low, even before the classification step to be described below;in the present invention, content of particles having a size of lessthan 150 μm in a water absorbent resin before classification ispreferably not more than 10% by weight, and more preferably not morethan 8% by weight.

<<The Classification Step>>

The above dried substance may be used as it is as a water absorbentresin, because generating amount of a fine powder thereof is less ascompared with conventional one, however, it may be used as a particulatewater absorbent resin after classification so as to have thepredetermined size. Such a classification may be carried out by using avibration sieve apparatus, an air-flow classification apparatus or thelike. A water absorbent resin obtained in this way may have variousshapes such as sphere-like, scale-like, indeterminate crushed form-like,fibrous, granular, bar-like, nearly spherical, flat-like shape or thelike.

After the above drying step of the above water-containing gel-likecross-linked polymer, particle size may be adjusted, if necessary, andpreferably specific particle size, to improve property in surfacecross-linking to be described later. The particle size can be adjustedas appropriate by polymerization (in particular, reversed phasesuspension polymerization), crushing, classification, agglomeration,fine particle recovering or the like.

Mass median particle size (D50) of a water absorbent resin is adjustedto from 200 to 600 μm, preferably from 200 to 550 μm, more preferably250 to 500 μm, more further preferably from 300 to 450 μm, andparticularly preferably from 350 to 400 μm. In addition, particles witha mass median particle size of smaller than 150 μm is preferably as lowas possible, and adjusted to usually from 0 to 5% by weight, morepreferably 0 to 3% by weight, and particularly preferably 0 to 1% byweight. Furthermore, particles with a mass median particle size oflarger than 850 μm is preferably as low as possible, and adjusted tousually from 0 to 5% by weight, more preferably 0 to 3% by weight, andparticularly preferably 0 to 1% by weight. Logarithmic standarddeviation (σζ) of the particle size distribution is preferably from 0.20to 0.40, preferably from 0.27 to 0.37, and more preferably from 0.25 to0.35.

<<The Surface Cross-Linking Step>>

A water absorbent resin obtained as above can be subjected to surfacecross-linking, if necessary, to improve absorption capacity againstpressure, so as to yield a surface cross-linked water absorbent resin.The surface cross-linking improves absorption capacity against pressure,fluid permeability, absorption rate of a water absorbent resin. For thesurface cross-linking, known surface cross-linking agents and knownmethods for surface cross-linking used in surface cross-linking of awater absorbent resin may be used.

As the above surface cross-linking agents, similar one used as across-linking agent, used in polymerization of the above monomercomponents may be used; and these cross-linking agents may be used aloneor two or more kinds in combination. Among these, ethylene glycoldiglycidyl ether, ethylene glycol, propylene glycol, butanediol,ethylene carbonate, polyethylene imine, polyamide amine-epichlorohydrinor the like is preferable. Using amount of the surface cross-linkingagent is preferably in a range of from 0.01% by weight to 10% by weight,and further preferably in a range of from 0.05% by weight to 5% byweight, relative to a water absorbent resin before surfacecross-linking.

The surface cross-linking agent is usually used as an aqueous solutionof the surface cross-linking agent. To dissolve the surfacecross-linking agent, water is preferably used as a solvent, and usingamount of water depends on kind or particle size or the like of a waterabsorbent resin, however, it is preferably over 0 and not more than 20parts by weight and more preferably in a range of from 0.5 to 10 partsby weight, relative to 100 parts by weight of solid content of a waterabsorbent resin.

In addition, in the case where a water absorbent resin and a surfacecross-linking agent are mixed, a water-soluble organic solvent (ahydrophilic organic solvent) may be used as a solvent if necessary. Asthe hydrophilic organic solvent, for example, lower alcohols such asmethyl alcohol, ethyl alcohol, n-propyl alcohol, isopropyl alcohol,n-butyl alcohol, isobutyl alcohol, t-butyl alcohol, and the like;ketones such as acetone and the like; ethers such as dioxane,tetrahydrofuran, alkoxypolyethylene glycol and the like; amides such asN,N-dimethylforamide and the like; sulfoxides such as dimethyl sulfoxideand the like is included. Using amount of the hydrophilic organicsolvent depends on kind or particle size or the like of a waterabsorbent resin, however, preferably from 0 to 20 parts by weight, morepreferably from 0 to 10 parts by weight, further preferably from 0 to 5parts by weight and particularly preferably from 0 to 1 part by weight,relative to 100 parts by weight of solid content of a water absorbentresin.

Using amount of a solution composed of the above water and thewater-soluble organic solvent (in the case of combined use) ispreferably not more than 50% by weight, further preferably within arange of from 0.5% by weight to 20% by weight and particularlypreferably within a range of from 1% by weight to 10% by weight,relative to the water absorbent resin without surface cross-linking.

Mixing of the above solution of the surface cross-linking agent into abase polymer (a particulate water absorbent resin before surfacecross-linking treatment) leads to swelling of a water absorbent resin bywater in the solution of the surface cross-linking agent or the like.Here, the swollen water absorbent resin is dried by heating. Heatingtemperature here (drying temperature) is preferably from 80 to 220° C.In addition heating time (drying time) is preferably from 10 to 120minutes.

It should be noted that these methods for surface cross-linking are alsodescribed in various European patents such as EP No. 0349240, EP No.0605150, EP No. 0450923, EP No. 0812873, EP No. 0450924, EP No. 0668080or the like; or various Japanese patents such as JP-A-7-242709,JP-A-7-224304 or the like; various U.S. patents such as U.S. Pat. No.5,409,771, U.S. Pat. No. 5,597,873, U.S. Pat. No. 5,385,983, U.S. Pat.No. 5,610,220, U.S. Pat. No. 5,633,316, U.S. Pat. No. 5,674,633, U.S.Pat. No. 5,462,972 or the like; and various international patents suchas WO99/42494, WO99/43720, WO99/42496 or the like, and these methods forsurface cross-linking are also applicable to the present invention.

It should be noted that during surface cross-linking or after surfacecross-linking, the agglomeration step may be set.

(A Water Absorbent Resin)

A water absorbent resin of the present invention is controlled to have,by the above surface cross-linking as an example of attaining method, anabsorption capacity against pressure (AAP) to 0.9% by weight of sodiumchloride, under 4.8 kPa, of preferably not less than 15 (g/g), morepreferably not less than 18 (g/g), and further preferably not less than20 (g/g). The upper limit thereof is not especially limited, however,preferably not more than 35 (g/g) and more preferably not more than 30(g/g), in view of other property balance.

A water absorbent resin of the present invention is controlled to have,by the above surface cross-linking as an example of attaining method, afluid permeability against pressure (flow conductivity of an aqueoussolution of 0.69% by weight of sodium chloride, SFC) of not less than5(×10⁻⁷·cm³·s·g⁻¹), more preferably not less than 10(×10⁻⁷·cm³·s·g⁻¹),further preferably not less than 30 (×10⁻⁷·cm³·s·g⁻¹), still furtherpreferably not less than 50 (×10⁻⁷·cm³·s·g⁻¹), particularly preferablynot less than 70 (×10⁻⁷·cm³·s·g⁻¹), and most preferably not less than100 (×10⁻⁷·cm³·s·g⁻¹). A measurement method for SFC may be pursuant to atest of saline flow conductivity (SFC) described in JP-A-9-509591.

A water absorbent resin of the present invention is controlled to have,by the above step as an example of attaining method, centrifugeretention capacity (CRC) to an aqueous solution of sodium chloride of0.90% by weight is preferably not less than 10 g/g, more preferably notless than 20 g/g, further preferably not less than 25 g/g andparticularly preferably not less than 30 g/g. CRC is preferably as highas possible, and the upper limit is not especially limited, however,preferably not more than 50 (g/g), more preferably not more than 45(g/g), and further preferably not more than 40 (g/g), in view of otherproperty balance.

As for a particle size of a water absorbent resin, ratio of particleswith a particle size of smaller than 150 μm is significantly reduced, bysubjecting to the grain refining step relevant to the present invention.Ratio of particles with a particle size of smaller than 150 μm ispreferably not more than 10% by weight, further preferably not more than5% by weight, more preferably not more than 2.5% by weight and mostpreferably not more than 1.5% by weight, relative to a water absorbentresin produced by a method of the present invention. It should be notedthat ratio of particles with a particle size of smaller than 150 μm iscalculated by a method in Examples to be described later.

<<Applications of a Water Absorbent Resin>>

A water absorbent resin obtained by a production method relevant to thepresent invention is applicable to various applications, due toexcellent absorption performance; for example, hygienic materials (bodyfluid absorption article) such as a disposable diaper or a sanitarynapkin, an incontinence pad, a wound protection material, a wound curingmaterial or the like; civil engineering and construction materials suchas construction material or water retention material for soil, watershielding material, packing material, gel water bag or the like;agriculture and gardening article; or the like.

EXAMPLES

The present invention will be described in more specifically below,based on Examples, however, the present invention should not be limitedthereto. It should be noted that, for convenience hereafter, “weightparts” may be described simply as “parts”, “litter” simply as “L”, and“milliliter” simply as “mL”. In addition, “% by weight” may be describedas “wt. %”. Further, a water absorbent resin was used (handled) under acondition of 25° C.±2° C. and a relative humidity of about 50%±5% RH. Inaddition, as a normal saline solution, an aqueous solution of 0.90% byweight of sodium chloride was used.

It should be noted that in the case where a commercial article such as awater absorbent resin in a disposable diaper is analyzed and when it isin a moisture absorbed state, it may be subjected to measurement afteradjustment of water content to about 5% by drying under reduced pressureas appropriate.

(Centrifuge Retention Capacity (CRC))

Into a bag (85 mm×60 mm) made of non-woven fabric (trade name: “HeatronPaper”, model GSP-22, manufactured by Nangoku Pulp Industry Co., Ltd.),0.2 g of a water absorbent resin was uniformly charged and heat sealed.Then this bag was immersed into a large excess (usually about 500 mL) ofthe normal saline solution adjusted at from 20° C. to 25° C. After 30minutes, the bag was pulled up and subjected to drainage using acentrifugal separator (Model H-122, a centrifugal separator,manufactured by KOKUSAN Co., Ltd.) at a centrifugal force of 250 G for 3minutes, as described in “edana ABSORBENCY II 441.1-99” to measure bagweight, W1 (g). In addition, the same procedure is carried out withoutusing a water absorbent resin to measure weight at this time, W2 (g).Then, using these weights, W1 and W2, absorption capacity (g/g) wascalculated according to the following formula:

absorption capacity(g/g)=(W1(g)−W2 (g))/(weight of the water absorbentresin(g))

<Absorption Capacity Against Pressure (AAP)>

Using an apparatus shown in FIG. 3, the 400-mesh wire gauze of stainlesssteel 101 (a mesh size of 38 μm), was welded to the bottom of a plasticsupporting cylinder 100 having an inner diameter of 60 mm, and 0.900 gof a water absorbent resin 102 was uniformly spread on the wire gauze;then a piston 103 and a load 104 each adjusted to exert a load of 4.83kPa (0.7 psi) uniformly on the water absorbent resin, given an outsidediameter slightly smaller than 60 mm, prevented from producing a gaprelative to the supporting cylinder, and enabled to produce anunobstructed vertical motion were mounted thereon sequentially in theorder mentioned, and the whole weight W6 (g) of the resultant measuringdevice was determined.

A glass filter 90 mm in diameter 106 (pore diameters: 100-120 μm: madeby Sogo Rikagaku Glass Manufactory K.K.) was placed inside a petri dish150 mm in diameter 105 and a physiological saline (20-25° C.) was addedto the petri dish till it rose to the same level as the upper surface ofthe glass filter. One filter paper 90 mm in diameter 107 (0.26 mm inthickness and 5 μm in retained particle diameter; made by Advantec ToyoK.K. and sold under the product name of “JIS P3801, No. 2”) was mountedon the physiological saline so as to have the surface thereof thoroughlywetted and the excess solution was removed.

The whole set of the above measurement apparatus was placed on thewetted filter paper, and the solution was subjected to absorption underload. After 1 hour, the whole set of the measurement apparatus waslifted up, to measure the weight thereof, W7 (g). Then, absorptioncapacity against pressure (g/g) was calculated from these weights, W6and W7, according to the following formula:

Absorption capacity against pressure=(W7(g)−W6(g))/(weight of the waterabsorbent resin(g))

<Extractable Polymer Content >

Into a 250-mL plastic container equipped with a cap, 184.3 g of a normalsaline solution is weighed, and 1.00 g of a water absorbent resin isadded into the aqueous solution, and stirred for 16 hours to extractextractables in the resin. This extracted solution is subjected tofiltering using a filter paper (trade name: JIS P3801, No. 2,manufactured by ADVANTEC TOYO MFS, Inc.; a thickness of 0.26 mm, and aretaining particle diameter of 5 μm), and 50.0 g of the resultingfiltrate was weighed as a measurement solution.

Firstly, by using only a normal saline solution, titration was carriedout using an aqueous solution of 0.1 N NaOH, till a pH of 10;subsequently by titration using an aqueous solution of 0.1N HCl, till apH of 2.7, blank titration amounts ([bNaOH] mL, [bHCl] mL) wereobtained. By similar titration operation also on the measurementsolution, titration amounts ([NaOH] mL, [HCl] mL) were obtained. Forexample, in the case where using a water absorbent resin composed ofacrylic acid and a salt thereof with known amounts, is used,extractables of the water absorbent resin (extracted water-solublepolymer as the main component) can be calculated, based on averagemolecular weight of the monomer and the titration amounts obtained bythe above operation, according to the following formula (2):

Extractables (% by weight)=0.1×(average molecularweight)×184.3×100×([HCl]−[bHCl])/1000/1.0/50.0  (2)

In addition, in the case of unknown amounts, the average molecularweight of the monomer is calculated, using neutralization ratedetermined by the titration (the following formula (3))

Neutralization rate(% bymol)=(1−([NaOH]−[bNaOH])/([HCl]−[bHCl]))×100  (3)

<Mass Median Particle Size, D50, and Logarithmic Standard Deviation(σζ)>

A water absorbent resin was sieved using JIS standard sieves with meshsize of 850 μm, 710 μm, 600 μm, 500 μm, 425 μm, 300 μm, 212 μm, 150 μm,106 μm, 75 μm and 45 μm to make a logarithm plot of residual percent. Itshould be noted that, depending of particle diameter of a waterabsorbent resin, sieves were added as appropriate, if necessary. In thisway, particle diameter corresponding to R=50% by mass was read as massmedian particle size, D50. In addition, logarithmic standard deviation(σζ) is represented by the following formula, and smaller value of σζmeans narrower particle size distribution.

σζ=0.5×ln(X2/X1)

(wherein, X1 and X2 are particle diameters when R=84.1% and R=84.1%,respectively)

Sieving was carried out by charging 10.0 g of a water absorbent resin inthe above JIS standard sieves (The IIDA TESTING SIEVE, manufactured byIIDA Seisakusyo Co., Ltd.: an inner diameter of 80 mm) and subjected toclassification for 5 minutes by a Ro-tap type sieve vibrator (an ES-65model sieve vibrator, manufactured by Iida Seisakusho Co., Ltd.).

It should be noted that mass median particle size, D50, is a particlediameter of a standard sieve corresponding to 50% by mass of wholeparticles, using standard sieves with certain mesh openings, asdescribed in U.S. Pat. No. 5,051,259 or the like.

<Ratio of Particles Having a Diameter of Smaller than 150 μm>

A water absorbent resin was sieved using a JIS standard sieve with amesh opening of 150 μm, and ratio of particles, which passed through theJIS standard sieve with a mesh size of 150 μm, to the total amount ofthe water absorbent resin was calculated by the following formula:

Ratio of particles having a diameter of smaller than 150 μm(%)=(weight(g) of a water absorbent resin passed through a sieve with a mesh sizeof 150 μm/total weight (g) of water absorbent resins sieved)×100

<Residence Amount of Gel and Residence Time of Gel>

Supply of gel to a meat chopper and rotation of the meat chopper werestopped at the same time, and gel amount (kg) left in the meat chopperwas weighed as residence amount of gel. In addition, residence time ofgel in the meat chopper was calculated by weighing charging amount(kg/h) of gel into the meat chopper, according to the following formula:

Residence time of gel(sec)=(residence amount of gel(kg)/charging amountof gel(kg/h))×3600(sec/h)

<Measurement of Residual Monomer>

Into 1000 g of deionized water, 0.5 g of a water absorbent resin wasadded and extracted for two hours under stirring with 4 cm stirrer, andsubsequently, the swollen gel-like water absorbent resin was filteredoff using a filter paper to analyze residual monomer amount in thefiltrate, with liquid chromatography. On the other hand, a calibrationcurve obtained by similar analysis of monomer standard solutions withknown concentrations was used as an external standard to determineresidual monomer amount in a water absorbent resin, in consideration ofdilution times of the filtrate.

<Solid Content>

In an aluminum cap with a diameter of the bottom surface of about 50 mm,1.00 g of a water absorbent resin was weighed to measure total weight ofthe water absorbent resin and the aluminum cap, W8 (g). Then, they weredried by standing still in an oven at an atmosphere temperature of 180°C. for three hours. After three hours, the water absorbent resin and thealuminum cup taken out from the oven were sufficiently cooled to roomtemperature in a desiccator to measure total mass of the water absorbentresin and the aluminum cap, W9 (g), after drying; solid content wasdetermined by the following formula:

Solid content(% by weight)=100−[(W8−W9)/(weight of a water absorbentresin particle(g))]×100

In addition, as for water-containing gel, solid content was determinedsimilarly as in the above measurement method except that drying time wasset to 16 hours.

Reference Example 1

(A) an aqueous solution of 48.5 wt. % of sodium hydroxide,

-   (B) an aqueous solution of 54.3 wt. % of acrylic acid, (C) a    solution composed of 9.33 wt. % of polyethylene glycol diacrylate    (an average molecular weight of 523), 0.30 wt. % of    hydroxycyclohexyl phenyl ketone, 0.37 wt. % of an aqueous solution    of 46 wt. % of diethylene triamine pentaacetic acid trisodium, 45.0    wt. % of acrylic acid and 45.0 wt. % of industrial pure water,    and (D) an aqueous solution of 3.0 wt. % of sodium persulfate were    each separately prepared, and each solution charged in a tank 31    storing the aqueous solution (A), a tank 32 storing the aqueous    solution (B), a tank 33 storing the solution (C), and a tank 34    storing the aqueous solution (D) (see FIG. 2). Solution temperature    in each of the tanks was set as follows: 33° C. for the aqueous    solution (A), 11° C. for the aqueous solution (B), 24° C. for the    solution (C), and 24° C. for the aqueous solution (D). It should be    noted that a pump 35 is installed at the each tank in FIG. 2.

By using a continuous polymerization apparatus shown in FIG. 2, and bysetting supplying amount (flowing amount) of each of the solutions asfollows: 17.5 kg/h for the aqueous solution (A); 40.0 kg/h for theaqueous solution (B); 1.7 kg/h for the solution (C); and 0.8 kg/h forthe aqueous solution (D), these solutions were mixed in the supplypipeline 37 to prepare an aqueous solution of a water-solubleunsaturated monomer (1). In this case, temperature of the aqueoussolution of the unsaturated monomer was 102° C. In the above mixing,nitrogen gas was introduced in a flowing rate of 200 mL/min into thesupply pipeline 37 at the more downstream side than the dispersionapparatus 36 in FIG. 2. Temperature of the aqueous solution of thewater-soluble unsaturated monomer (1) in the supply pipeline 37 wasstabilized at 97° C. Amount of dissolved oxygen (a) in the aqueoussolution of the water-soluble unsaturated monomer (1) in the supplypipeline 37 was 8.6 mg/L. It should be noted that a degassing apparatusis installed on the supply pipeline 37 in FIG. 2.

The aqueous solution of the water-soluble unsaturated monomer (1) in thesupply pipeline 37 was subsequently supplied to the belt polymerizationapparatus 38, as a polymerization system, to carry out polymerization.The belt polymerization apparatus 38 is equipped with the endless belt39 with a length of 3.8 m and a width of 60 cm, which is coated with afluorocarbon resin at the surface thereof, installed with a UV lamp onthe belt 39, heated at about 100° C. at the bottom surface side of thebelt 39 and the surrounding of the belt polymerization apparatus 8, andmaintained at a moisturized state, and provided with an air suctionpipeline to recover evaporated water, at the center part. Amount ofdissolved oxygen (b) in the aqueous solution of the water-solubleunsaturated monomer (1) after purging dissolved oxygen, in supplying tothe polymerization step, was 3.5 mg/L. The aqueous solution of thewater-soluble unsaturated monomer (1) was continuously supplied onto theabove belt 39 from the supply pipeline to carry out polymerization, toobtain the belt-like polymer gel 40.

The resulting belt-like water-containing gel-like cross-linked polymer(a1) (with a thickness of 5-10 mm) 10 was continuously crushed intoparticulate form using the meat chopper 42 (model TB32, manufactured byHiraga Kosakusyo Co., Ltd.). Rotation number of the meat chopper herewas 105 rpm, charging amount of gel into meat chopper was 50.9 kg/h; andresidence amount of gel in the meat chopper was 0.36 kg.

The particulate water-containing gel-like cross-linked polymer (a1),obtained by crushing using the meat chopper, was spread on a wire gauzeof stainless steel with a mesh size of 850 μm, to be subjected to dryingby hot air at 180° C. for 30 minutes, and then a dried substance waspulverized using a roll mill to obtain a particulate water absorbentresin. Centrifuge retention capacity (CRC) of the particulate waterabsorbent resin was 34 g/g.

The resulting water absorbent resin was classified using a JIS standardsieve with a mesh size of 160 μm to obtain a polyacrylic acid(salts)-based water absorbent resin particle (A) having a D50 of 97 μmand a particle diameter of equal to or smaller than 160 μm. In addition,centrifuge retention capacity (CRC) of the water absorbent resinparticle (A) was 32 g/g.

Example 1

In a KRC kneader (model S2, manufactured by Kurimoto, Ltd.), 2.7 kg/h ofthe water absorbent resin particle (A) obtained in Reference Example 1,and 2.7 kg/h of ion-exchanged water were mixed to obtain thewater-containing gel-like cross-linked polymer (b1) with a solid contentof 50% by weight, which was then continuously charged and crushed in themeat chopper, together with the water-containing gel-like cross-linkedpolymer (a1) (polymer gel having a solid content of 53% by weight)obtained similarly as in Reference Example 1. Total charging amount ofgel (water-containing gel-like cross-linked polymers (a1) and (b1)) intothe meat chopper here was 56.3 kg/h, and residence amount of gel in themeat chopper was 0.27 kg.

The water-containing gel-like cross-linked polymers (a1) and (b1)crushed using the meat chopper were spread on a wire gauze of stainlesssteel with a mesh size of 850 μm, to be subjected to drying by hot airat 180° C. for 30 minutes, and then a dried substance was pulverizedusing a roll mill to obtain a particulate water absorbent resin. Ratioof particles, having a particle diameter of smaller than 150 μm, of theresulting particulate water absorbent resin was 7.1% by weight.

By further classification and blending of the resulting water absorbentresin using JIS standard sieves with mesh size of 850 μm, 600 μm, 300μm, 150 μm, and 45 μm, a water absorbent resin powder (1) was obtained,which had D50 of 461 μm; ratio of particles, having a particle diameterof equal to or larger than 850 μm, of 0% by weight; ratio of particles,having a particle diameter of equal to or larger than 600 μm and smallerthan 850 μm, of 28% by weight; and ratio of particles, having a particlediameter of smaller than 150 μm, of 7.1% by weight; and a logarithmicstandard deviation (σζ) of 0.364.

To 100 parts by weight of the resulting water absorbent resin powder(1), a solution of a surface treatment agent, composed of mixed solutioncontaining 0.3 part by weight of 1,4-butanediol, 0.5 part by weight ofpropylene glycol, and 2.7 parts by weight of deionized water, wasuniformly mixed. The water absorbent resin mixed with the solution ofthe surface treatment agent was subjected to heat treatment at arbitrarytime, using a heating apparatus equipped with a stirring blade and ajacket (a jacket temperature of 210° C.). After the heat treatment, theresulting water absorbent resin was subjected to passing through the JISstandard sieve with a mesh size of 850 μm to obtain surface cross-linkedparticulate water absorbent resin (1). Various properties of theparticulate water absorbent resin (1) were shown in Table 1.

Example 2

In a KRC kneader (model S2, manufactured by Kurimoto, Ltd.), 0.05 kg/hof the water absorbent resin particle (A) obtained in Reference Example1, and 5.0 kg/h of ion-exchanged water were mixed to obtain thewater-swollen gel (a water-containing gel-like cross-linked polymer(b2)) with a solid content of 1% by weight, which was then continuouslycharged and crushed in the meat chopper, together with thewater-containing gel-like cross-linked polymer (a1) obtained similarlyas in Reference Example 1. Total charging amount of gel ((a1)+(b2)) intothe meat chopper here was 55.95 kg/h, and residence amount of gel in themeat chopper was 0.23 kg.

Gel obtained by crushing using the meat chopper was subjected to dryingand pulverizing similarly as in Example 1 to obtain a particulate waterabsorbent resin. Ratio of particles, having a particle diameter ofsmaller than 150 μm, of the resulting particulate water absorbent resinwas 7.8% by weight, and ratio of particles, having a particle diameterof not less than 850 μm was 0% by weight.

The resulting water absorbent resin was subjected to surfacecross-linking treatment and sieving using a JIS standard sieve with amesh size of 850 μm, similarly as in Example 1 to obtain particulatewater absorbent resin (2). Various properties of the particulate waterabsorbent resin (2) were shown in Table 1.

Example 3

Ina KRC kneader (model S2, manufactured by Kurimoto, Ltd.), 2.7 kg/h ofthe water absorbent resin particle (A) obtained in Reference Example 1,and 1.8 kg/h of ion-exchanged water were mixed to obtain awater-containing gel-like cross-linked polymer (b3) with a solid contentof 60% by weight, which was then continuously charged and crushed in themeat chopper, together with the water-containing gel-like cross-linkedpolymer (a1) (polymer gel having a solid content of 53% by weight)obtained similarly as in Reference Example 1. Total charging amount ofgel into the meat chopper here was 55.4 kg/h, and residence amount ofgel in the meat chopper was 0.30 kg.

Gel obtained by crushing using the meat chopper was subjected to dryingand pulverizing similarly as in Example 1 to obtain a particulate waterabsorbent resin. Ratio of particles, having a particle diameter ofsmaller than 150 μm, of the resulting particulate water absorbent resinwas 8.9% by weight, and ratio of particles, having a particle diameterof not less than 850 μm was 0% by weight.

The resulting water absorbent resin was subjected to surfacecross-linking treatment and sieving using a JIS standard sieve with amesh size of 850 μm, similarly as in Example 1 to obtain particulatewater absorbent resin (3). Various properties of the particulate waterabsorbent resin (3) were shown in Table 1.

Example 4

Water-containing gel-like cross-linked polymers (a2) (a solidconcentration of 54.2% by weight) was obtained similarly as in ReferenceExample 1, except that composition of the solution (C) in ReferenceExample 1 was changed to 5.60 wt. % of polyethylene glycol diacrylate(an average molecular weight of 523), 0.30 wt. % of hydroxycyclohexylphenyl ketone, 0.37 wt. % of an aqueous solution of 46 wt. % ofdiethylene triamine pentaacetic acid trisodium, 45.0 wt. % of acrylicacid and 48.73 wt. % of industrial pure water.

Similarly as in Example 1, in a KRC kneader (model S2, manufactured byKurimoto, Ltd.), 2.7 kg/h of the water absorbent resin particle (A)obtained in Reference Example 1, and 2.7 kg/h of ion-exchanged waterwere mixed to obtain a water-containing gel-like cross-linked polymer(b1) (swollen gel), which was then continuously charged and crushed inthe meat chopper, together with the water-containing gel-likecross-linked polymer (a2). Total charging amount of gel into the meatchopper here was 55.2 kg/h, and residence amount of gel in the meatchopper was 0.33 kg.

Gel obtained by crushing using the meat chopper was subjected to dryingand pulverizing similarly as in Example 1 to obtain a particulate waterabsorbent resin. Ratio of particles, having a particle diameter ofsmaller than 150 μm, of the resulting particulate water absorbent resinwas 6.6% by weight, and ratio of particles, having a particle diameterof not less than 850 μm was 0% by weight.

The resulting water absorbent resin was subjected to surfacecross-linking treatment and sieving using a JIS standard sieve with amesh size of 850 μm, similarly as in Example 1, to obtain particulatewater absorbent resin (4).

Example 5

Water-containing gel-like cross-linked polymers (a3) (a solidconcentration of 43.0% by weight) was obtained similarly as in ReferenceExample 1, except that the concentration of the aqueous solution (B) inReference Example 1 was changed to 33% by weight.

Then, in a KRC kneader (model S2, manufactured by Kurimoto, Ltd.), 2.7kg/h of the water absorbent resin particle (A) obtained in ReferenceExample 1, and 2.7 kg/h of ion-exchanged water were mixed to obtain awater-containing gel-like cross-linked polymer (b1), which was thencontinuously charged and crushed in the meat chopper, together with thewater-containing gel-like cross-linked polymer (a3). Total chargingamount of gel into the meat chopper here was 58.4 kg/h, and residenceamount of gel in the meat chopper was 0.22 kg.

Gel obtained by crushing using the meat chopper was subjected to dryingand pulverizing similarly as in Example 1 to obtain a particulate waterabsorbent resin. Ratio of particles, having a particle diameter ofsmaller than 150 μm, of the resulting particulate water absorbent resinwas 6.3% by weight, and ratio of particles, having a particle diameterof not less than 850 μm was 0% by weight.

The resulting water absorbent resin was subjected to surfacecross-linking treatment and sieving using a JIS standard sieve with amesh size of 850 μm, similarly as in Example 1, to obtain particulatewater absorbent resin (5).

Comparative Example 1

A crushed substance of polymer gel (water-containing gel-likecross-linked polymer (a1)) obtained by polymerization in ReferenceExample 1, and a water-swollen gel-like substance (water-containinggel-like cross-linked polymer (b1)) obtained by mixing in Example 1,using a KRC kneader (manufactured by Kurimoto, Ltd.) were weighed in thesame predetermined amount, and were spread on a wire gauze of stainlesssteel with a mesh size of 850 μm, to be subjected to drying by hot airat 180° C. for 30 minutes. Then a dried substance was pulverized using aroll mill to obtain a particulate water absorbent resin. Ratio ofparticles, having a particle diameter of smaller than 150 μm, of theresulting particulate water absorbent resin was 14.4% by weight, andratio of particles, having a particle diameter of not less than 850 μmwas 0% by weight.

The resulting water absorbent resin was subjected to surfacecross-linking treatment and sieving using a JIS standard sieve with amesh size of 850 μm, similarly as in Example 1, to obtain a comparativeparticulate water absorbent resin (1).

Comparative Example 2

A particulate water absorbent resin was obtained, without the additionof swollen gel (water-containing gel-like cross-linked polymer (b1)),similarly as in polymerization in Reference Example 1. By furtherclassification and blending of the resulting particulate water absorbentresin using JIS standard sieves with mesh size of 850 μm, 600 μm, 300μm, 150 μm, and 45 μm, a comparative water absorbent resin powder (2)was obtained.

The resulting comparative water absorbent resin powder (2) was subjectedto surface cross-linking treatment and sieving using a JIS standardsieve with a mesh size of 850 μm, similarly as in Example 1, to obtain acomparative particulate water absorbent resin (2).

Comparative Example 3

Only polymer gel (water-containing gel-like cross-linked polymer (a3))obtained by polymerization in Example 5, without the addition of swollengel (water-containing gel-like cross-linked polymer (b1)), in Example 5,was crushed using a meat chopper. Then, similarly as in Example 5, thecrushed substance spread on a wire gauze of stainless steel with a meshsize of 850 μm, to be subjected to drying by hot air at 180° C. for 30minutes. Then a dried substance was pulverized using a roll mill toobtain a particulate water absorbent resin. Ratio of particles, having aparticle diameter of smaller than 150 μm, of the resulting particulatewater absorbent resin was 8.6% by weight, and ratio of particles, havinga particle diameter of not less than 850 μm was 0% by weight.

The resulting water absorbent resin was subjected to surfacecross-linking treatment and sieving using a JIS standard sieve with amesh size of 850 μm, similarly as in Example 1, to obtain a comparativeparticulate water absorbent resin (3).

(Result)

Various properties of the above particulate water absorbent resins (1)to (5), and the comparative particulate water absorbent resins (1) to(3) were shown in Table 1.

TABLE 1 Various conditions in gel crushing Particulate water absorbentresin Retention Retention Solid content of Solid content of aftercrushing using roll mill amount time water-containing water-containingRate of particles having of gel of gel gel (a) gel (b) a particlediameter of (kg) (sec) (% by weight) (% by weight) smaller than 150 μm(%) Reference Example 1 0.36 25.5 53.0 — — Example 1 Particulate 0.2717.3 53.0 50.0 7.1 water absorbent resin (1) Example 2 Particulate 0.2314.8 53.0 0.99 7.8 water absorbent resin (2) Example 3 Particulate 0.3019.5 53.0 60.0 8.9 water absorbent resin (3) Example 4 Particulate 0.3321.5 54.2 50.0 6.6 water absorbent resin (4) Example 5 Particulate 0.2213.6 43.0 50.0 6.3 water absorbent resin (5) Comparative Comparative0.36 25.5 53.0 50.0 14.4 Example 1 particulate water absorbent resin (1)Comparative Comparative 0.36 25.5 53.0 — 11.3 Example 2 particulatewater absorbent resin (2) Comparative Comparative 0.28 19.0 43.0 — 8.0Example 3 particulate water absorbent resin (3) Particulate waterabsorbent resin after surface treatment Absorption Absorption Rate ofparticles having capacity capacity against Extractables a particlediameter of (g/g) pressure (g/g) (% by mass) smaller than 150 μm (%)Reference Example 1 — — — — Example 1 Particulate 27.3 24.1 13.3 1.3water absorbent resin (1) Example 2 Particulate 27.7 24.6 12.8 1.5 waterabsorbent resin (2) Example 3 Particulate 27.3 23.4 13.9 1.0 waterabsorbent resin (3) Example 4 Particulate 33.8 22.1 19.5 0.8 waterabsorbent resin (4) Example 5 Particulate 27.5 25.5 11.9 1.0 waterabsorbent resin (5) Comparative Comparative 26.6 22.1 12.4 2.6 Example 1particulate water absorbent resin (1) Comparative Comparative 27.0 23.013.7 1.5 Example 2 particulate water absorbent resin (2) ComparativeComparative 27.5 25.6 11.0 1.2 Example 3 particulate water absorbentresin (3)

(Supplemental Explanation on Table)

In Examples 1 to 3, wherein polymer gel (a water-containing gel-likecross-linked polymer (a3)) is subjected to grain refining in thepresence of water-swollen gel (a water-containing gel-like cross-linkedpolymer (b1)), not only treatment amount is improved due to reducedresidence time of gel by 24-42% (Reference Example 1, 25.5 seconds;Example 1-5, 14.8-21.5 seconds), but also a fine particle having aparticle diameter of smaller than 150 μm after crushing by roll mill isreduced by 37-22%, and further absorption capacity or absorptioncapacity against pressure is also improved, and in particular,extractables are also reduced, in the case where solid content ofwater-swollen gel is low, as compared with Comparative Example 2,wherein a water-containing gel-like cross-linked polymer (a3) issubjected to grain refining without using water-swollen gel.

Similar effect is observed; namely, even in polymer gel having low solidcontent (a water-containing gel-like cross-linked polymer (a3)), as isfound by comparison between Example 5 and Comparative Example 3,presence of water-swollen gel (a water-containing gel-like cross-linkedpolymer (b1)) not only enhances treatment amount due to reducedresidence time of gel, but also reduces a fine particle having aparticle diameter of smaller than 150 μm. It should be noted that, bycomparison between Examples 1 to 3 and Example 5, effect of the presentinvention is found to be fulfilled in a region where solid content ofwater-containing gel-like cross-linked polymer (a) is high.

In Comparative Example 1, wherein water-swollen gel (a water-containinggel-like cross-linked polymer (b1)) is mixed after grain refining ofpolymer gel (a gel-like cross-linked polymer (a1)), in Example 1,absorption capacity or absorption capacity against pressure is also low,as compared with Example 1 or Comparative Example 2 (wherein awater-containing gel-like cross-linked polymer (b1) is not used).

INDUSTRIAL APPLICABILITY

A production method relevant to the present invention is capable ofcontrolling a particle size (for example, reduction of a fine powder) orimproving fundamental property (for example, absorption capacity,absorption capacity against pressure, extractables), withoutparticularly using new sub-raw materials or additives, and in low priceand in high productivity, and is thus preferable as a method forproducing a water absorbent resin.

This application is based on Japanese patent application No. 2006-267567filed in Japan on Sep. 29, 2006, and the disclosed contents thereof areincorporated herein by reference in its entirety.

1. A method for producing a water absorbent resin particle comprising:subjecting an aqueous solution of an unsaturated monomer tocross-linking polymerization to produce a water-swellable,water-containing gel-like cross-linked polymer (a); subjecting thewater-swellable, water-containing gel-like cross-linked polymer (a) tograin refining to produce a grain refined gel; drying the grain refinedgel to yield a dried substance; and pulverizing the dried substance,wherein, in the step of grain refining the water-swellable,water-containing gel-like cross-linked polymer (a), a water-swellable,water-containing gel-like cross-linked polymer (b), having solid contentor centrifuge retention capacity different from solid content orcentrifuge retention capacity of the cross-linked polymer (a), issubjected to coexistence.
 2. The method according to claim 1, furthercomprising a surface cross-linking step, after the drying step.
 3. Themethod according to claim 1, wherein residence time of a mixture of thecross-linked polymer (a) and the cross-linked polymer (b) inside a grainrefining apparatus used in the grain refining step is within 30 seconds.4. The method according to claim 1, wherein the grain refining apparatusis a screw extruder.
 5. The method according to claim 1, wherein solidcontent of the water-swellable, water-containing gel-like cross-linkedpolymer (a) subjected to grain refining is equal to or higher than 40%by weight.
 6. The method according to claim 1, wherein solid content ofthe water-swellable, water-containing gel-like cross-linked polymer (b)is lower as compared with the water-swellable, water-containing gel-likecross-linked polymer (a).
 7. The method according to claim 1, whereinsolid content of the water-swellable, water-containing gel-likecross-linked polymer (b) is from 0.1 to 10% by weight.
 8. The methodaccording to claim 1, wherein centrifuge retention capacity of thewater-swellable, water-containing gel-like cross-linked polymer (b) islower as compared with the water-swellable, water-containing gel-likecross-linked polymer (a).
 9. The method according to claim 1, whereinsolid content of a mixture of the water-swellable, water-containinggel-like cross-linked polymers (a) and (b) is from 40 to 60% by weight.10. The method according to claim 1, wherein the water-swellable,water-containing gel-like cross-linked polymer (b) is obtained byrecycling of the production step for a water absorbent resin.
 11. Themethod according to claim 1, wherein the water-swellable,water-containing gel-like cross-linked polymer (b) is obtained from apolymer gel in a cross-linking polymerization step.
 12. The methodaccording to claim 1, wherein the water-swellable, water-containinggel-like cross-linked polymer (b) is obtained by the addition of waterto a water absorbent resin particle subjected to a classification step.13. The method according to claim 1, wherein the water-swellable,water-containing gel-like cross-linked polymer (b) is obtained bywashing a production apparatus of a water absorbent resin with water.14. The method according to claim 2, wherein residence time of a mixtureof the cross-linked polymer (a) and the cross-linked polymer (b) insidea grain refining apparatus used in the grain refining step is within 30seconds.
 15. The method according to claim 2, wherein the grain refiningapparatus is a screw extruder.
 16. The method according to claim 3,wherein the grain refining apparatus is a screw extruder.
 17. The methodaccording to claim 14, wherein the grain refining apparatus is a screwextruder.
 18. The method according to claim 2, wherein solid content ofthe water-swellable, water-containing gel-like cross-linked polymer (a)subjected to grain refining is equal to or higher than 40% by weight.19. The method according to claim 3, wherein solid content of thewater-swellable, water-containing gel-like cross-linked polymer (a)subjected to grain refining is equal to or higher than 40% by weight.20. The method according to claim 4, wherein solid content of thewater-swellable, water-containing gel-like cross-linked polymer (a)subjected to grain refining is equal to or higher than 40% by weight.